WO2023100084A1 - Ensemble filtre - Google Patents

Ensemble filtre Download PDF

Info

Publication number
WO2023100084A1
WO2023100084A1 PCT/IB2022/061566 IB2022061566W WO2023100084A1 WO 2023100084 A1 WO2023100084 A1 WO 2023100084A1 IB 2022061566 W IB2022061566 W IB 2022061566W WO 2023100084 A1 WO2023100084 A1 WO 2023100084A1
Authority
WO
WIPO (PCT)
Prior art keywords
panel
filtering
baffle
inlet
filter group
Prior art date
Application number
PCT/IB2022/061566
Other languages
English (en)
Inventor
Giorgio Girondi
Original Assignee
Ufi Innovation Center S.R.L.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ufi Innovation Center S.R.L. filed Critical Ufi Innovation Center S.R.L.
Publication of WO2023100084A1 publication Critical patent/WO2023100084A1/fr

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
    • B01D46/0036—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions by adsorption or absorption
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0039—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with flow guiding by feed or discharge devices
    • B01D46/0041—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with flow guiding by feed or discharge devices for feeding
    • B01D46/0043—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with flow guiding by feed or discharge devices for feeding containing fixed gas displacement elements or cores
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0039—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with flow guiding by feed or discharge devices
    • B01D46/0047—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with flow guiding by feed or discharge devices for discharging the filtered gas
    • B01D46/0049—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with flow guiding by feed or discharge devices for discharging the filtered gas containing fixed gas displacement elements or cores
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
    • B01D46/12—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces in multiple arrangements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
    • B01D46/58—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in parallel

Definitions

  • the present invention relates to a filter group for a fluid .
  • the filter group is speci fically suitable for performing air filtration operations .
  • the context to which the present invention pertains is that of filtering groups , preferably, but not necessarily, of the automotive field .
  • filtering groups which are connectable , by means of speci fic channels and speci fic mani folds , to operating groups of a vehicle or to speci fic spaces of the vehicle , so as to filter the fluid and prevent said operating groups or said spaces from being reached by fluids containing undesired particles .
  • Such filtering groups housed in a vehicle are required to be suitable for performing an ef fective and ef ficient filtration of the fluid, occupying a space as small as possible and avoiding obstructing the outflow of the fluid towards the operating group or the desired space .
  • the filter group of the present invention is preferably particularly suitable for being housable in narrow installation spaces .
  • Figures la, lb, 1c and Id show a diagram of a preferred embodiment of the filter group of the present invention, in a top perspective view with separate parts , a bottom perspective view with separate parts , a front view and a longitudinal sectional view, respectively;
  • FIGS. 2a, 2b, 2c and 2d show a diagram of a preferred embodiment of the filter group of the present invention, in a top perspective view with separate parts , a bottom perspective view with separate parts , a front view and a longitudinal sectional view, respectively;
  • FIG. 3a, 3b, 3c and 3d show a diagram of a preferred embodiment of the filter group of the present invention, in a top perspective view with separate parts , a bottom perspective view with separate parts , a front view and a longitudinal sectional view, respectively;
  • FIG. 4a, 4b, 4c and 4d show a diagram of a preferred embodiment of the filter group of the present invention, in a top perspective view with separate parts , a bottom perspective view with separate parts , a front view and a longitudinal sectional view, respectively;
  • FIG. 5a, 5b, 5c and 5d show a diagram of a preferred embodiment of the filter group of the present invention, in a top perspective view with separate parts , a bottom perspective view with separate parts , a front view and a longitudinal sectional view, respectively;
  • FIG. 6a, 6b, 6c and 6d show a diagram of a preferred embodiment of the filter group of the present invention, in a top perspective view with separate parts , a bottom perspective view with separate parts , a front view and a longitudinal sectional view, respectively;
  • FIGS. 7a, 7b, 7c and 7d show a diagram of a preferred embodiment of the filter group of the present invention, in a top perspective view with separate parts , a bottom perspective view with separate parts , a front view and a longitudinal sectional view, respectively;
  • FIGS. 8a, 8b, 8c and 8d show a diagram of a preferred embodiment of the filter group of the present invention, in a top perspective view with separate parts , a bottom perspective view with separate parts , a front view and a longitudinal sectional view, respectively;
  • FIGS. 9a and 9b show a diagram of a preferred embodiment of the filter group of the present invention, in a top perspective view with separate parts and a longitudinal sectional view, respectively;
  • FIG. 10a and 10b show a diagram of a preferred embodiment of the filter group of the present invention, in a top perspective view with separate parts and a longitudinal sectional view, respectively;
  • FIG. 11 shows a diagram of a preferred embodiment of the filter group of the present invention, in a top perspective view with separate parts ;
  • FIG. 12a, 12b, 12c and 12d depict further diagrammatic embodiments of the filter group of the present invention.
  • FIG. 14 shows a detailed embodiment of a filter group of the present invention, according to a preferred embodiment
  • FIG. 15 depicts a detail of a further embodiment of the filter group of the present invention, according to a preferred embodiment ;
  • FIG. 16a and 16b depict further embodiments and some relative details of the filter group of the present invention, according to a preferred embodiment ;
  • FIG. 19a, 19b, 19c, 19d and 19e depict further embodiments and some relative details of the filter group of the present invention, according to a preferred embodiment .
  • reference numeral 1 indicates a filter group in accordance with the present invention .
  • Said filter group 1 is crossable under filtration by a fluid .
  • said filter 1 is crossable under filtration by air .
  • the filter group 1 comprises a filtration region R in which the filtration of the fluid, and therefore the separation from the fluid of undesired substances or particles , occurs .
  • the filtration region R extends in length between an inlet area IN through which fluid to be filtered flows , and an outlet area OUT through which filtered fluid flows .
  • the filter group 1 of the present invention is suitable for being highly flexible in the design, construction, and manufacturing thereof , so as to allow the mutual positioning of the inlet area IN and outlet area OUT according to speci fic needs .
  • the filter group 1 extends along a longitudinal axis X-X, along a transverse axis Y-Y and along a vertical axis V-V .
  • the longitudinal axis X-X extends in a linear direction .
  • the longitudinal axis X-X extends in a curvilinear direction ( as shown by way of example in Figure 11 , Figure 12a and Figure 13e ) .
  • the longitudinal axis X-X extends in a broken direction ( as shown by way of example in Figure 12b and Figure 12d) .
  • the longitudinal axis X-X extends in a mixed manner, having linear segments and curvilinear segments ( as shown by way of example in Figure 12c ) .
  • the transverse axis Y-Y is transverse to the longitudinal axis X-X .
  • the transverse axis Y-Y is orthogonal to the longitudinal axis X-X .
  • the transverse axis Y-Y extends in a linear direction .
  • the transverse axis Y-Y extends in a curvilinear direction ( as shown by way of example in Figures 13a, 13b, 13c, 13d, 13e and 13 f ) .
  • the transverse axis Y-Y extends in a broken direction .
  • the transverse axis Y-Y extends in a mixed manner, having linear segments and curvilinear segments .
  • the vertical axis V-V extends from the longitudinal axis X-X, transversely thereto . Preferably, it extends transversely to the longitudinal axis X-X and transversely to the transverse axis Y-Y . Preferably, the vertical axis V-V is orthogonal to an imaginary plane in which both the longitudinal axis X-X and the transverse axis Y-Y lie .
  • the vertical axis V-V extends in a linear direction .
  • the vertical axis V-V extends in a curvil inear direction .
  • the vertical axis V-V extends in a broken direction .
  • the vertical axis V-V extends in a mixed manner, having linear segments and curvilinear segments .
  • the filter group 1 has such a shape as to extend in length along said longitudinal axis X-X and said transverse axis Y-Y, for example , by positioning the inlet area IN and the outlet area OUT at two opposite ends along the longitudinal axis X-X, or by positioning the inlet area IN at a longitudinal end and the outlet area OUT at a transverse end .
  • the filter group 1 comprising a central cavity C and the filtration region R extends about the central cavity C .
  • the filter group 1 has a substantially tubular shape , having a substantially cylindrical or conical or f rustoconical shape ( as shown by way of example in Figures 13a, 13b, 13c, 13d, 13e and 13 f ) .
  • the longitudinal axis X-X extends parallel along the tubular extension of the filter group 1 , while the transverse axis Y-Y extends in a substantially circumferential direction, and the vertical axis V-V extends in a radial direction .
  • the inlet area IN and the outlet area OUT are positioned at two axial ends along the longitudinal axis X-X: the filter group 1 operates as an "axial filter”.
  • the inlet area IN and the outlet area OUT are positioned at two longitudinally opposite ends, i.e., mutually spaced apart along the longitudinal axis X-X.
  • Such a first embodiment is shown as an example in Figure 13a.
  • the longitudinal axis X-X extends substantially radially with respect to the tubular extension of the filter group 1, while the transverse axis Y-Y extends in a substantially circumferential direction, and the vertical axis V-V extends parallel along the tubular extension of the filter group 1.
  • the inlet area IN and the outlet area OUT are positioned at two radial ends along the longitudinal axis X-X, i.e., at least one of the two areas corresponds to the central cavity C: the filter group 1 operates as a "radial filter".
  • the outlet area OUT corresponds to the central cavity C, while the inlet area IN is radially spaced apart outside the tubular filter group 1: the filter group 1 operates as an outer-inner radial filter.
  • the filter group 1 operates as an outer-inner radial filter.
  • the inner cavity C delimits a fluid passage having a varying passage section .
  • the inner cavity C delimits a fluid passage with an increasing passage section along the axis of the cavity itsel f .
  • said cavity is obtained by stacking filtering panels 3 and baf fle panels 4 of a di f ferent annular shape .
  • this solution allows facilitating the circulation of fluid through the filter group 1 in the distal portions from the outlet area, in particular in the distal portions from the axial end of the filter group 1 facing the outlet area, thus improving the distribution of the flow under filtration along the axis of the filter group 1 .
  • the filter group 1 comprises :
  • a filtering panel 3 which is crossable by the fluid under filtration in a direction substantially orthogonal to the extension thereof ;
  • baf fle panel 4 a baf fle panel 4 ;
  • the filtering panel 3 extends with respect to an imaginary plane F which is crossable by the fluid under filtration in a direction substantially orthogonal to the imaginary plane F .
  • the baf fle panel 4 is made of a fluid permeable material .
  • the filtering panel 3 extends in a substantially planar manner .
  • both the longitudinal axis X-X and the transverse axis Y-Y lie on said imaginary plane F, therefore the shape of the imaginary plane F ( i . e . , linear or curvilinear or serrated) is a function of the shape of the longitudinal axis X-X and the transverse axis Y-Y .
  • the filtering panel 3 is crossable under filtration by the fluid in the thickness thereof .
  • the filtering panel 3 is crossable under filtration by the fluid in a direction substantially parallel to the vertical axis V-V .
  • the inlet chamber 5 is open in a region which is proximal to the inlet area IN and is closed in a region which is proximal to the outlet area OUT .
  • the inlet chamber 5 is thus open only and exclusively in a region which is proximal to the inlet area IN, while it is closed in a region which is proximal to the outlet area OUT so that the fluid is forced to cross the filtering panel 3 .
  • the coupling of the filtering panel 3 to the baf fle panel 4 is such as to define an inlet chamber 5 shaped so as to comprise a first inlet area I I corresponding to a first section substantially orthogonal to the imaginary plane F in a region which is proximal to the inlet area IN and a second inlet area 12 corresponding to a second section substantially orthogonal to the imaginary plane F in a region which is distal from the inlet area IN .
  • the first inlet area I I is greater than the second inlet area 12 .
  • the inlet chamber 5 has a decreasing passage section with a monotonous course along the extension thereof .
  • the coupling of the filtering panel 3 to the baf fle panel 4 is such as to define an inlet chamber 5 having a larger passage section close to the inlet area IN and a smaller passage section close to the outlet area OUT .
  • baf fle panel 4 for example , comprising speci f ic portions with a tapered course or comprising a greater number of components suitable for allowing the flow of the fluid in a region which is proximal to the inlet area IN with respect to the number of components present in a region which is proximal to the outlet area OUT .
  • Such a particular preferred embodiment is such as to allow a better access of the fluid into the inlet chamber 5 and is such as to make the filtering panel 3 work as homogeneously as possible .
  • the filter group 1 comprises a pair of baf fle panels 4 which are permeable to the fluid, positioned at the two opposite faces of the filtering panel 3 .
  • the first baf fle panel 4 and the filtering panel 3 define said inlet chamber 5.
  • the filtering panel 3 and the second baf fle panel 4 define an outlet chamber 6 which is open in a region proximal to the outlet area OUT and is closed in a region proximal to the inlet area IN .
  • the filter group 1 comprises a pair of filtering panels 3 , wherein the baf fle panel 4 is positioned in the space between two filtering panels so that said inlet chamber 5 is defined between the first filtering panel 3 and the baf fle panel 4 , and so that an outlet chamber 6 is defined between the second filtering panel 3 and the baf f le panel 4 .
  • said outlet chamber 6 is open in a region which is proximal to the outlet area OUT and is closed in a region which is proximal to the inlet area IN .
  • the coupling of the filtering panel 3 to the baf fle panel 4 is such as to define an outlet chamber 6 shaped so as to comprise a first outlet area 01 corresponding to a first section substantially orthogonal to the imaginary plane F in a region which is proximal to the inlet area IN and a second outlet area 02 corresponding to a second section substantially orthogonal to the imaginary plane F in a region which is proximal to the outlet area OUT .
  • the first outlet area 01 is smaller than the second outlet area 02 .
  • the outlet chamber 6 has an increasing passage section with a monotonous course along the extension thereof .
  • the coupling of the filtering panel 3 to the baf fle panel 4 is such as to define an outlet chamber 6 having a smaller passage section close to the inlet area IN and a larger passage section close to the outlet area OUT .
  • this is achieved by particular shapes of the baf fle panel 4 , for example , comprising speci f ic portions with a tapered course or comprising a greater number of components suitable for allowing the flow of the fluid in a region which is proximal to the outlet area OUT with respect to the number of components present in a region which is proximal to the inlet area IN .
  • Such a particular preferred embodiment is such as to improve the circulation of the filtered fluid exiting from the filtering panel 3 , as well as such as to make said filtering panel 3 work as homogeneous ly as possible .
  • the outlet chamber 6 is complementary to the inlet chamber 5 .
  • the baf fle panel 4 delimits speci fic, complementary, outlet channels 600 .
  • the inlet area IN and the outlet area OUT are spatially positioned as a function of the shape or of the position of the baf fle panel 4 which delimits the outlet chamber 6 ( as diagrammatically exempli fied in Figures 10a and 10b ) .
  • the filter group 1 comprises a plurality of filtering panels 3 and a plurality of baf fle panels 4 stacked parallel to the direction of the vertical axis V-V .
  • the filter group 1 comprises a plurality of filtering panels 3 and a plurality of baf fle panels 4 stacked parallel to the direction of the vertical axis V-V so as to form a plurality of inlet chambers 5 and a plurality of outlet chambers 6 crossed in parallel by the working fizid .
  • the filter group 1 comprises a plurality of filtering panels 3 and a plurality of baf fle panels 4 stacked parallel to the direction of the vertical axis V-V so as to form a plurality of inlet chambers 5 comprising a plurality of inlet channels 500 and a plurality of outlet chambers 6 comprising a plurality of outlet channels 600 crossed in parallel by the working fluid .
  • the inlet chambers 5 and the outlet chambers 6 have the same height .
  • the filter group 1 comprises a plurality of inlet chambers 5 and a plurality of outlet chambers 6 having di f ferent heights .
  • the filter group 1 comprises a plurality of filtering panels 3 and a plurality of baf fle panels 4 stacked parallel to the direction of the vertical axis V-V so as to form a plurality of inlet chambers 5 and outlet chambers 6 arranged so as to form two filtering portions which are crossable in series by the working fluid .
  • each filtering portion comprises a plurality of inlet chambers 5 and outlet chambers 6 crossed in parallel by the working fluid .
  • a plurality of filtering panels 3 and baf fle panels 4 are preferably alternated along said vertical axis V-V so as to identi fy a multiplicity of inlet chambers 5 and outlet chambers 6 .
  • panel in the present description means a component which mainly extends along two preferential directions .
  • the filtering panel 3 and the baf fle panel 4 have the same substantially square shape .
  • the filter group 1 resulting from the stacking of a plurality of filtering panels 3 and baf fle panels 4 has a cubic shape .
  • the filtering panel 3 and the baf fle panel 4 have the same substantially rectangular shape .
  • the filter group 1 resulting from the stacking of a plurality of filtering panels 3 and baf fle panels 4 has a parallelepiped shape .
  • the filtering panel 3 and the baf fle panel 4 have the same discoidal shape .
  • the filter group 1 resulting from the stacking of a plurality of filtering panels 3 and baf fle panels 4 has a cylindrical shape .
  • the filtering panel 3 is a sheet-like filtering medium made of a porous filtering material .
  • the filtering panel 3 is a filtering medium made of non-woven fabric .
  • the filtering panel 3 is made from a non-woven fabric comprising polyester and/or polypropylene and/or polyamide and/or polyacrylate and/or viscose and/or rayon fibers and/or any combination thereof .
  • the filtering panel 3 is a depth filtering septum made in the form of a flat sheet .
  • the filtering panel 3 is made of a non-woven fabric having a permeability between 150 and 950 mm/ s , preferably between 550 and 700 mm/ s (measured at 200 Pa ) .
  • the filtering panel 3 is singlelayer .
  • the filtering panel 3 is of the multi-layer type .
  • the filtering panel 3 comprises a first filtering layer of non-woven fabric, with a permeability between 750 and 900 mm/ s ( at 200 Pa ) , coupled to a second filtering layer of non-woven fabric with a lower permeability, between 150 and 200 mm/ s ( at 200 Pa ) .
  • the filtering panel 3 comprises a third filtering layer positioned between the two outer layers and having an intermediate permeability, between 250 and 300 mm/ s ( at 200 Pa ) .
  • the filtering panel 3 contains adsorbent substances therein, such as activated carbons and/or ion exchange resins and/or zeolites .
  • the filtering panel 3 comprises a filtering layer suitable for filtering particles and an adsorbent layer suitable for adsorbing gaseous contaminants .
  • the filtering layer is positioned upstream of the adsorbent layer with respect to the fluid crossing direction .
  • the adsorbent layer comprises a plurality of adsorbent substances such as activated carbons and ion exchange resins .
  • the filtering panel 3 comprises a filtering layer suitable for filtering particles and a plurality of adsorbent layers comprising respective adsorbent elements.
  • the filtering panel 3 has an ISO5011 filtering efficiency greater than 99% (ISO FINE) .
  • the filtering panel 3 has a thickness between 0.5 and 3.5 millimeters (measured according to ASTM D5729 - 1997) , preferably the filtering panel 3 has a thickness between 1.5 millimeters and 2.8 millimeters.
  • the baffle panel 4 is a sheet-like element made of a permeable material.
  • the baffle panel 4 is such as to have a permeable structure, said baffle panel 4 being made, for example, of a fibrous material, a spongy material, a composite material or a sintered material.
  • the baffle panel 4 is a sheet-like element made of a material belonging to the family of plastic materials.
  • the baffle panel 4 is a sheet-like element made of a permeable fibrous material. [00115] In accordance with a preferred embodiment, the baffle panel 4 is a sheet-like element made of a permeable cellulose-based material.
  • the baffle panel 4 is made of a material comprising an adsorbent substance, preferably comprising activated carbons and/or ion exchange resins and/or zeolites.
  • the baffle panel 4 is a sheet-like element made of a material comprising adsorbent substances, preferably comprising activated carbons and/or ion exchange resins and/or zeolites .
  • the baffle panel 4 comprises adsorbent substances at least on the surface facing the inlet chamber 5 of the filter group 1.
  • the baffle panel 4 comprises adsorbent substances on the surface facing the outlet chamber 6 of the filter group 1.
  • the baffle panel 4 has a thickness of less than 1 millimeter, preferably between 0.1 and 0.5 millimeters, preferably the baffle panel has a thickness of 0.2 millimeters.
  • the baffle panel 4 is processed by means of a thermoforming process.
  • the baffle panel 4 is processed by molding.
  • the filtering panel 3 has a filter efficiency class.
  • the baffle panel 4 has a baffle efficiency class.
  • Effective class means the class established by a respective standard, as a function of the intended use of the filter group and thus also as a function of the type of fluid to be filtered: examples of efficiency classes are preferably described in standard EN1822 (for HEPA filters) or standard ISO5011 (for air filters) .
  • a reference efficiency class is thus established.
  • the filtering panel 3 has a filter efficiency class and the baffle panel 4 has a baffle efficiency class, preferably in proximal classes to said reference efficiency class.
  • the filtering panel 3 has a filter permeability.
  • the baffle panel 4 has a baffle permeability.
  • the permeability values are measured according to standard EN ISO 9073.
  • both the filtering panel 3 and the baffle panel 4 are crossable by the fluid.
  • the baffle efficiency class is higher than the filter efficiency class.
  • the baffle efficiency class is higher than the filter efficiency class which is in turn higher than, or equal to, the reference efficiency class.
  • the filtering panel 3 has a filter efficiency class equal to E10, according to standard EN 1822.
  • the baffle panel 4 has a higher baffle efficiency class, while the reference efficiency class is lower than, or equal to, the filter efficiency class.
  • the filtering panel 3 has a filter efficiency class equal to H13, according to standard EN 1822.
  • the baffle panel 4 has a higher efficiency class, while the reference efficiency class is lower than, or equal to, the filter efficiency class.
  • efficiency class means permeable elements having a certain filtration efficiency with respect to a specific type of powder when performing tests according to the indications of standard ISO 5011.
  • the filtering panel 3 and the baffle panel 4 belong to the same filtering efficiency class both having a filtration efficiency higher than 99% with ISOFINE powder.
  • the filtering panel 3 and the baffle panel 4 belong to the same filtering efficiency class both having a filtration efficiency higher than 99.5% with ISOFINE powder.
  • the filtering panel 3 and the baffle panel 4 have a different filtering efficiency class having a filtration efficiency equal to 99.5% with ISOFINE powder and equal to 99.0% with ISOFINE powder, respectively .
  • the filtering panel 3 and the baffle panel 4 have a different filtering efficiency class having a filtration efficiency equal to 99.9% with ISOFINE powder and equal to 99.5% with ISOFINE powder, respectively .
  • the baffle permeability is lower than the filter permeability.
  • the baffle permeability is higher than the filter permeability.
  • the baffle permeability is substantially equal to the filter permeability .
  • the baffle efficiency class is lower than the filter efficiency class.
  • the filter efficiency class is higher than the baffle efficiency class, which is in turn higher than, or equal to, the reference efficiency class.
  • the filtering panel 3 has an efficiency class equal to E10, according to standard EN 1822.
  • the baffle panel 4 has a lower efficiency class than E10, but higher than, or equal to, the reference efficiency class.
  • the filtering panel 3 has an efficiency class equal to H13, according to standard EN 1822.
  • the baffle panel 4 has a lower efficiency class than H13, but higher than, or equal to, the reference efficiency class.
  • the baffle permeability is lower than the filter permeability.
  • the baffle permeability is higher than the filter permeability.
  • the baffle permeability is substantially equal to the filter permeability .
  • the fluid crosses the filtering panel 3 or the baffle panel 4 with less resistance .
  • the fluid crosses the filtering panel 3 with less resistance than the baf fle panel 4 . In particular, this takes place under the initial operating conditions of the f ilter group 1 .
  • the baf fle panel 4 promotes the outflow of fluid towards the filtering panel 3 , while , However, being in turn permeable to the fluid thus suitable in turn for performing a filtering action thereon .
  • the fluid flows into the inlet chamber 5 and is forced across the filtering panel 3 .
  • the fluid flowing into the inlet chamber 5 crosses and is filtered by the baf fle panel 4 .
  • the filtering panel 3 comprises an inlet filter edge 31 and an outlet filter edge 32 .
  • the filtering panel 3 comprises side edges 34 which connect the inlet filter edge 31 to the outlet filter edge 32 .
  • the inlet filter edge 31 is proximal to , preferably faces , the inlet area IN, and the outlet filter edge 32 is proximal to, preferably faces, the outlet area OUT.
  • the baffle panel 4 preferably comprises an inlet baffle edge 41 and an outlet baffle edge 42.
  • the baffle panel 4 comprises side baffle surfaces 44.
  • the inlet baffle edge 41 is proximal to, preferably faces, the inlet area IN and the outlet baffle edge 42 is proximal to, preferably faces, the outlet area OUT.
  • said outlet baffle edge 42 sealingly engages the filtering panel 3.
  • the outlet baffle edge 42 sealingly engages the outlet filter edge 32 closing the inlet chamber 5.
  • the outlet baffle edge 42 comprises an outlet edge portion 420 comprising an outlet housing cavity 421 in which the outlet filter edge 32 is housed.
  • the outlet filter edge 32 is preferably clamped into the outlet housing cavity 421.
  • the outlet edge portion 420 preferably closes and blocks the flow of the fluid crossing the thickness of the filtering panel 3 .
  • the baf fle panel 4 sealingly engages the filtering panel 3 , with the purpose of defining the outlet chamber 6 , even by means of the inlet baf fle edge 41 .
  • the baf fle panel 4 comprises , in a region which is proximal to the outlet area OUT , a portion shaped so as to have the sealing engagement on the first fi ltering panel 3 superimposed, along the vertical axis , to the sealing engagement on the second filtering panel 3 , thus fluidically closing the inlet chamber 5.
  • the inlet baf fle edge 41 engages the filtering panel 3 with an inlet edge portion 410 comprising an inlet housing cavity 411 in which the inlet filter edge 31 of said filtering panel is housed 3 .
  • the baf fle panel 4 comprises , in a region proximal to the inlet area INT , a portion shaped so as to have the sealing engagement on the first filtering panel 3 aligned along the vertical axis with the sealing engagement on the second filtering panel 3 , thus fluidically closing the outlet chamber 6 , but allowing the inlet into the inlet chamber 5 ( as shown by way of example in Figures 17a, 17b and 17c ) .
  • the inlet filter edge 31 is clamped into the inlet housing cavity 411 .
  • the inlet edge portion 410 preferably closes and blocks the flow of the fluid crossing the thickness of the filtering panel 3 .
  • the side baf fle surfaces 44 sealingly engage the filtering panel 3 .
  • the side baf fle surfaces 44 sealingly engage the side edges 34 of the filtering panel 3 .
  • the inlet chamber 5 is thus closed on three sides at the side baf fle surfaces 44 and at the outlet baf fle edge 42 .
  • the outlet chamber 6 is thus closed on three sides at the side baf fle surfaces 44 and at the inlet baf fle edge 41 .
  • said side baf fle surfaces 44 extend in height substantially parallel to the vertical axis V-V .
  • each side baf fle surface 44 comprises a support foot 440 substantially parallel to the imaginary plane F, suitable for sealingly engaging the filtering panel 3 .
  • the inlet baf fle edge 41 and/or the outlet baf fle edge 42 comprise respective support steps substantially parallel to the imaginary plane F suitable for sealingly engaging the filtering panel 3 .
  • the side baf fle surfaces 44 comprise a protruding side portion 441 suitable for extending beyond the filtering panel 3 on the opposite side with respect to that in which the coupling of the baf fle panel 4 to the filtering panel 3 defines the inlet chamber 5 .
  • the protruding side portion 441 of a baf fle panel 4 is suitable for engaging the subsequent baf fle panel 4 allowing the stacking thereof in the vertical direction .
  • the protruding side portion 441 of a baf fle panel 4 is suitable for engaging the subsequent baf fle panel 4 so that the mutual engagement between two baf fle panels 4 is sealed ( as shown by way of example in Figure 15 ) .
  • the baf fle panel 4 is positioned in the space between two filtering panels 3 , so as to sealingly engage both the first filtering panel 3 and the second filtering panel 3 with the side baf fle surfaces 44 .
  • the side baf fle surface 44 is shaped so as to have the sealing engagement on the first filtering panel 3 aligned, along the vertical axis V-V, with the sealing engagement on the second filtering panel 3 .
  • the side baf fle surfaces 44 also have a preferred shape similar to that shown with reference to the outlet regions in Figures 18a, 18b and 18c .
  • the baf fle panel 4 is shaped comprising a plurality of alternate walls 40 suitable for defining a plurality of inlet channels 500 in the inlet chamber 5 .
  • each inlet channel 500 comprises an inlet mouth 501 proximal to the inlet area IN and a filtration region 502 facing the filtering panel 3 .
  • the fluid is channeled at the inlet along each inlet channel 500 , up to the filtration region 502 facing the filtering panel 3 .
  • each alternate wall 40 is connected to the next alternate wall in a top portion 401 and is connected to the previous alternate wall in a bottom portion 402 .
  • said top portions 401 and/or said bottom portions 402 are mutually j oined to each other in an arcuate manner .
  • said top portions 401 and/or said bottom portions 402 comprise speci fic support planes .
  • the respective bottom portions 402 of the baf fle panel 4 rest on the filtering panel 3 .
  • the respective bottom portions 402 of the baf fle panel 4 generally rest on a filtering panel 3 .
  • the respective top portions 401 are engaged by a filtering panel 3 .
  • the baf fle panel 4 also preferably acts as a reinforcement and support element for the filtering panels 3 .
  • the inlet channels 500 delimited by the baf fle panel 4 have an open inlet end facing the inlet area IN and a closed outlet end close to the outlet area OUT . Said outlet ends are closed by appropriate closing elements such as portions of adhesive used for coupling a baf fle panel 4 to a filtering panel 3 , for example .
  • the outlet channels 600 delimited by the baf fle panel 4 have a closed inlet end close to the inlet area IN and an open outlet end facing the outlet area OUT . Said inlet ends are closed by appropriate closing elements such as portions of adhesive used for coupling a baf fle panel 4 to a filtering panel 3 , for example .
  • the inlet channels 500 delimited by the baf fle panel 4 have lengths which are di f ferent from one another, comprising primary inlet channels 500 which extend from the inlet area IN to a region which is proximal to the outlet area OUT .
  • the inlet channels 500 delimited by the baf fle panel 4 comprise auxiliary inlet channels 500 which extend from the inlet area IN to a region which is distal to the outlet area OUT .
  • the baf fle panel 4 comprises primary inlet channels 500 and auxiliary inlet channels 500 .
  • the inlet channels 500 delimited by the baf fle panel 4 have a variable pitch along the transverse axis Y-Y ( as exempli fied in Figure 12a, for example ) .
  • the pitch of the inlet channels 500 is a function of the very nature of the aforesaid channels .
  • the pitch of the inlet channels 500 is a function of the length of the inlet channels 500 having baf fle panel portions with a greater number of channels in the region in which there are inlet channels 500 of a length shorter with respect to baf fle panel portions where primary inlet channels 500 of a greater length are present .
  • the baf fle panel 4 transversely alternates primary inlet channels and auxiliary inlet channels ( as shown by way of example in Figure 13 f ) .
  • Such a preferred embodiment is particularly used on embodiments with filtering panels 3 having an extension with respect to longitudinal axes X-X or with respect to transverse axes Y-Y of a non-linear type , for example curvilinear .
  • the same considerations described for the inlet channels 500 are present for the outlet channels 600 defined by the baf fle panel 4 : for example , where the inlet channels 500 have a course which decreases when decreasing in section, the outlet channels 600 expand when expanding the section thereof ; for example , auxiliary outlet channels are at the location of primary inlet channels , and vice versa, primary outlet channels are at the location of auxiliary inlet channels .
  • the inlet channels 500 have a constant section which is di f ferent from the constant section of the outlet channel s 600 .
  • each inlet channel 500 is greater than the passage section of each outlet channel 600 .
  • the distribution of the fluid flowing towards the filtering panel 3 is improved and the dust accumulation ef fect by each filtering panel 3 of the filter group 1 is maximi zed, also reducing the pressure drops .
  • the filtering panel 3 is in the shape of a disc .
  • the baf fle panel 4 is in the shape of a disc .
  • the filtering panel 3 and the baf fle panel 4 are mutually engaged defining an inlet chamber 5 of an annular shape .
  • the filtering panel 3 and the baf fle panel 4 are mutually engaged to define an outlet chamber 6 of an annular shape .
  • the baf fle panel 4 has channels oriented in the radial direction .
  • the baf fle panel 4 defines inlet channels 500 oriented in the radial direction .
  • the baf fle panel 4 defines outlet channels 600 oriented in the radial direction ( as shown in Figures 13b to 13 f ) .
  • the baf fle panel 4 defines passage channels with a spiral geometry in the inlet chamber 5 and/or in the outlet chamber 6 ( as shown in Figure 13e ) .
  • the alternate walls 40 have an incident course , so as to delimit inlet channels 500 with a tapered course .
  • the alternate walls 40 have an incident course , so as to delimit outlet channels with a tapered course .
  • the baf fle panel 4 or the alternate walls 40 comprise baf fle elements 409 , so as to delimit inlet channels 500 with a tapered course .
  • the baf fle elements 409 are suitable for acting as a chute for the fluid towards the filtering panel 3 .
  • the filter group 1 comprises a container body 2 suitable for containing the filtration region R, containing the at least one filtering panel 3 and the at least one baffle panel 4 .
  • the container body has such a shape as to identi fy the inlet area IN and the outlet area OUT to fluidically connect them by means of the filtration region R, inside which the filtering panels 3 and the baf fle panels 4 are housed .
  • the container body 2 compri ses a perimeter gasket 20 which extends about the at least one filtering panel 3 and the at least one baf fle panel 4 , so as to define the inlet area IN .
  • the baf fle panels 4 are shown substantially planar ; although, according to the needs , they have the wavy shape described so as to be suitable for defining the respective inlet channels 500 and the respective outlet channels 600 described above as shown in Figures 14 to 19e .
  • the filter group largely ful fills the purpose of the present invention, overcoming issues typical of the prior art .
  • the filter group is suitable for filtering the fluid in a highly ef fective and ef ficient manner, not acting as an obstacle to the flow of the fluid, but rather favoring the motion thereof in a substantially main connection direction between the inlet area and the outlet area .
  • the filter group has a wide inlet surface and a wide outlet surface while having however wide filtering surfaces .
  • the baf fle panel favors the flow of the fluid at the inlet and favors the outflow of the fluid at the outlet .
  • the baf fle panel since the baf fle panel is permeable , it minimi zes the pressure drops imposed on the system in which the filter group is installed .
  • the baf fle panel distributes the flow rate of the fluid which strikes the filtering panel , improving the use of the available filtering surface .
  • the baf fle panel gives solidity to the filter group .
  • the baf fle panel compri ses an inlet edge which engage the filtering panel , improving the fluid dynamics of the filter group, in particular, reducing the pressure drops at the entrance to the inlet chamber .
  • the baf fle panel compri ses an outlet edge which engage the filtering panel , improving the fluid dynamics of the filter group, in particular, reducing the pressure drops at the exit of the outlet chamber .
  • the baf fle panel comprises edge portions which engage the filtering panel , simpli fying the separation between each inlet chamber and each outlet chamber .
  • the filter group is modular and is simply adaptable to the design needs by taking advantage of all the above advantages .
  • the filter group allows to easily modulate the available filtering surface by selecting the number of filtering panels , baf fle panels and/or by acting on the dimensions thereof , such as , for example , on the length thereof .
  • the behavior of the filtering panel is easily and faithfully determinable so as to produce ef fective and ef ficient filter groups .
  • performance losses of the filtering panel conventionally due to bending/def ormation operations , are avoided .
  • the filtering panel is used in the form of a flat sheet , similar to the experimental conditions in which it is tested and developed .
  • the filtering panels do not require multiple production operations , such as , for example , filtering panels comprising pleated paper filters .
  • the production costs of the filtering panels and filter group are highly low .
  • the filtering panels have a porous and permeable structure , thus managing to accumulate the contaminant in the thicknes s thereof .
  • the passage channels are formed on the baf fle panel , keeping the structure of the filtering panel , on which no bending and/or deformation operations have to be performed, simple .
  • the filtering panels have a permeable , bulky, and relatively thick filtering structure , which is utili zable for accumulating contaminants in the thickness of the filtering panel .
  • the filtering panels may have a multilayer structure , for example , comprising at least one filtering layer and at least one adsorbent layer, thus allowing to obtain a multi functional filtering structure with relative simplicity, thus avoiding folding processes .
  • the filtering panel is made of hydrophobic synthetic fibers , preferably polypropylene .
  • the resistance of the filter group to the treatment with humid and/or dropletcontaining air is increased .
  • the baf fle panel has mainly the purpose of defining, with its positioning with and coupling to the filtering panel , the inlet chamber, and possibly the outlet chamber, but at the same time is also adapted to perform the filtering action .
  • the fluid is filterable by both the filtering panel and the baf fle panel .
  • a blockage of the filtering panel is ef fectively managed by continuing the filtering action through the baf fle panel .
  • the presence of adsorbent substances on the baf fle panel allows maximi zing the utili zation of the available spaces in order to ensure the amount of adsorbent substance useful to ensure a desired adsorption capacity of the fi lter group .
  • the filtering panel and the baf fle panel are made of di f ferent permeable materials .
  • for making the baf fle panel it is possible to select cost-ef fective materials as compared to the material of the filtering panel or the material of the baf fle panels which are impermeable to the fluid, thus reducing the costs associated with the production of the filter group .
  • the particle fi ltration and gas adsorption properties are assigned to the filtering panel and the baf fle panel , respectively, they being workable according to respective production processes and easy to stack and mutually couplable for defining the described structure of the filter group .

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Fluid-Pressure Circuits (AREA)
  • Lubrication Details And Ventilation Of Internal Combustion Engines (AREA)
  • Filtration Of Liquid (AREA)

Abstract

L'invention concerne un groupe filtre (1) comprenant une région de filtration (R) s'étendant entre une zone d'entrée (IN) à travers laquelle le fluide à filtrer s'écoule, et une zone de sortie (OUT) à travers laquelle s'écoule le fluide filtré. Le groupe filtre (1) s'étend le long d'un axe longitudinal (X-X), le long d'un axe transversal (Y-Y) et, en hauteur, le long d'un axe vertical (V-V). En outre, le groupe filtre (1) comprend : Un panneau filtrant (3) qui s'étend par rapport à un plan imaginaire (F) et est apte à être réticulé par le fluide sous filtration dans une direction sensiblement orthogonale au plan imaginaire (F), le panneau filtrant (3) a une classe d'efficacité de filtre ; un panneau déflecteur (4) ayant une classe d'efficacité de déflecteur ; une chambre d'entrée (5) définie entre le panneau filtrant (3) et le panneau déflecteur (4), la chambre d'entrée (5) étant ouverte dans une région proximale à la zone d'entrée (IN) et étant fermée dans une région proximale à la zone de sortie (OUT). Dans le groupe filtre (1) selon la présente invention, la classe d'efficacité du filtre diffère de la classe d'efficacité du déflecteur.
PCT/IB2022/061566 2021-11-30 2022-11-30 Ensemble filtre WO2023100084A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT102021000030314 2021-11-30
IT102021000030314A IT202100030314A1 (it) 2021-11-30 2021-11-30 Gruppo filtro

Publications (1)

Publication Number Publication Date
WO2023100084A1 true WO2023100084A1 (fr) 2023-06-08

Family

ID=80461680

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/IB2022/061566 WO2023100084A1 (fr) 2021-11-30 2022-11-30 Ensemble filtre

Country Status (2)

Country Link
IT (1) IT202100030314A1 (fr)
WO (1) WO2023100084A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116874076A (zh) * 2023-08-16 2023-10-13 浙江中昌水处理科技有限公司 一种具有自清洁能力的反硝化生物滤池脱氮除磷系统

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE456676C (de) * 1928-02-29 K & Th Moeller G M B H Gas- und Luftfilter mit Glasfaeden als Filterstoff
WO1986001430A1 (fr) * 1984-09-06 1986-03-13 Klas Jakobsson Agencement de filtre pour le lavage d'un milieu gazeux
WO2001064311A1 (fr) * 2000-02-28 2001-09-07 Clair Finance Ab Dispositif et procede de filtration d'air
US20090113862A1 (en) * 2005-12-16 2009-05-07 Connor Michael J Volume-Efficient Filter
US20210129063A1 (en) * 2019-11-01 2021-05-06 Guild Associates Inc. Filter for Purifying an Air Stream

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE456676C (de) * 1928-02-29 K & Th Moeller G M B H Gas- und Luftfilter mit Glasfaeden als Filterstoff
WO1986001430A1 (fr) * 1984-09-06 1986-03-13 Klas Jakobsson Agencement de filtre pour le lavage d'un milieu gazeux
WO2001064311A1 (fr) * 2000-02-28 2001-09-07 Clair Finance Ab Dispositif et procede de filtration d'air
US20090113862A1 (en) * 2005-12-16 2009-05-07 Connor Michael J Volume-Efficient Filter
US20210129063A1 (en) * 2019-11-01 2021-05-06 Guild Associates Inc. Filter for Purifying an Air Stream

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116874076A (zh) * 2023-08-16 2023-10-13 浙江中昌水处理科技有限公司 一种具有自清洁能力的反硝化生物滤池脱氮除磷系统
CN116874076B (zh) * 2023-08-16 2024-01-30 浙江中昌水处理科技有限公司 一种具有自清洁能力的反硝化生物滤池脱氮除磷系统

Also Published As

Publication number Publication date
IT202100030314A1 (it) 2023-05-30

Similar Documents

Publication Publication Date Title
US7407533B2 (en) Active filter element for end face incident flow
US3490211A (en) High efficiency particulate air filter
US6315805B1 (en) Single or multi-ply filter medium for air filtration and a filter element made therefrom
US6953124B2 (en) Filter element with end face inlets and discharge outlets
KR100531673B1 (ko) 여과기 요소
US8251231B2 (en) Corrugated or pleated flat material
US4479874A (en) Convoluted plural layer filter assembly
ZA200104274B (en) Multi-layer filter element.
CN102413897A (zh) 用于具有安装凸缘延伸部的燃气涡轮机的过滤器组件
WO2023100084A1 (fr) Ensemble filtre
CN102015062A (zh) 具有安全元件的空气滤清器
EP1932576A1 (fr) Elément de filtre doté d'un revêtement de charbon actif
KR102138010B1 (ko) 수처리 장치의 복합 필터
WO2023100085A1 (fr) Ensemble filtre
US20070017879A1 (en) Filtration cartridge and process for filtering a slurry
US20240001275A1 (en) Filter group
WO2022112905A1 (fr) Groupe filtre
WO2022112904A1 (fr) Groupe filtre
WO2023089579A1 (fr) Ensemble filtre
WO2023126808A1 (fr) Groupe filtre
CN216726253U (zh) 过滤器组
CN218107123U (zh) 过滤器组件
CN117138472A (zh) 过滤器组
CN117138481A (zh) 过滤器组
CN116764351A (zh) 过滤器组件

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 22822224

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2022822224

Country of ref document: EP

Effective date: 20240701